Method for biologically removing nitrogen from wastewater

• US 5,213,681 A
• Filed: 09/09/1991
• Issued: 05/25/1993
• Est. Priority Date: 09/09/1991
• Status: Expired due to Fees

• Current Assignee: Peter Kos
• Original Assignee: T Kruger Incorporated
• Inventors: Kos, Peter
• Primary Examiner(s): Wyse, Thomas
• Application Number:
  US07/756,440
• Time in Patent Office: 624 Days
• Field of Search: 210/605, 210/607, 210/610, 210/614, 210/620-631, 210/903, 210/906
• US Class Current: 210/605
• CPC Class Codes: C02F 3/308 Biological phosphorus removal
• CPC Class Codes: Y10S 210/903 Nitrogenous
• CPC Class Codes: Y10S 210/906 Phosphorus containing

Abstract

The present invention relates to a system and method for biologically removing nitrogen from wastewater. Both the system and method entails forming a mixed liquor and transferring the mixed liquor to a series of nitrogen removal stages. Each nitrogen removal stage includes both anoxic and aerobic treatment zones. Mixed liquor is recycled back and forth between the anoxic and aerobic treatment zone of each stage. Because of this basic flow scheme, the process gives rise to a high reactor rate and highly efficient nitrogen removal process.

Claims

1. An activated sludge process for biologically removing BOD and nitrogen from wastewater comprising the steps of:

(a) forming mixed liquor;

(b) transferring the mixed liquor through a first nitrogen removal stage by directing the mixed liquor into and through first anoxic and aerobic treatment zones including maintaining the mixed liquor under anoxic conditions within the first treatment zone for a specified period to permit denitrifying organisms to reduce a portion of the nitrates and nitrites present in the mixed liquor to elemental nitrogen, transferring a portion of the mixed liquor from the first anoxic zone to the first aerobic zone and aerating the mixed liquor for a sufficient time period for nitrifying organisms to convert a portion of the ammonia and organic nitrogen in the mixed liquor into nitrates and nitrites, and circulating the mixed liquor back and forth between the first anoxic zone and the first aerobic zone of the first nitrogen removal stage to effectuate denitrification and nitrification;

(c) transferring mixed liquor from the first nitrogen removal stage to a second nitrogen removal stage having a second anoxic zone and a second aerobic zone, and circulating the mixed liquor back and forth between the second anoxic zone and the second aerobic zone of the second stage to effectuate further denitrification and nitrification;

(d) transferring the mixed liquor treated in the first and second nitrogen removal stages to a final clarifier where settled sludge is separated from purified supernatant; and

(e) recycling at least a portion of the settled sludge to form the mixed liquor.

2. The activated sludge process according to claim 1 wherein the step of transferring the mixed liquor through a plurality of nitrogen removal stages includes first introducing the mixed liquor into the anoxic zone in each nitrogen removal stage.

3. The activated sludge process according to claim 2 wherein the step of transferring mixed liquor from one nitrogen removal stage to the next nitrogen removal stage includes transferring the mixed liquor from the first anoxic zone to the second anoxic zone.

4. The activated sludge process according to claim 3 wherein the first aerobic zone in the first nitrogen removal stage is disposed in a closed circulation mode so that mixed liquor transferred from the first anoxic zone to the first aerobic zone is recycled back to the first anoxic zone before being transferred to the second nitrogen removal stage.

5. The activated sludge process according to claim 1 wherein the mixed liquor is transferred through a plurality of nitrogen removal stages and the process includes initially introducing the mixed liquor into the first anoxic zone of the first nitrogen removal stage, and for each subsequent nitrogen removal stage, first introducing the mixed liquor into the aerobic zone.

6. The activated sludge process according to claim 5 wherein the step of transferring the mixed liquor from one nitrogen removal stage to the next nitrogen removal stage includes transferring the mixed liquor from an aerobic zone of a preceding nitrogen removal stage to an aerobic zone of a subsequent nitrogen removal stage.

7. The activated sludge process according to claim 6 wherein the anoxic zone in each nitrogen removal stage, except the first nitrogen removal stage is disposed in a closed loop so that mixed liquor transferred from the aerobic zone to the anoxic zone of a nitrogen removal stage is recycled back to the aerobic zone before proceeding to the next stage.

8. The activated sludge process according to claim 1 further including treating the mixed liquor in an anaerobic zone before transferring the mixed liquor to the first nitrogen removal stage and maintaining the mixed liquor in said anaerobic zone for a sufficient period to effect selection of phosphate storing organisms.

9. The activated sludge process according to claim 8 wherein the anaerobic zone comprises a plurality of hydraulically distinct sections.

10. The process according to claim 1 wherein the recycle from one zone to another in each nitrogen removal stage is 100%-200% of the wastewater influent to the process.

11. The activated sludge process of claim 1 including the step of adding methanol to at least one of the anoxic treatment zones.

12. The method of claim 1 including the step of adding a fermented product to the process.

13. The method of claim 12 including the step of adding the fermented product to the first anoxic zone of the first nitrogen removal stage.

14. The method of claim 1 wherein in recycling the mixed liquor back and forth between anoxic and oxic zones, the mixed liquor is recycled from an oxic zone to an anoxic zone and wherein the method includes holding the mixed liquor being recycled from at least one oxic zone in an exhauster holding tank for a selected time period and exhausting the dissolved oxygen associated with the mixed liquor before the mixed liquor is returned to the anoxic zone.

15. The method of claim 14 including the step of holding the mixed liquor in the dissolved oxygen exhauster holding tank for a time period sufficient to reduce the dissolved oxygen level of the mixed liquor therein to below 0.6 ppm.

16. The method of claim 1 wherein the formed mixed liquor includes BOD and wherein the method includes a step of averting the complete depletion of BOD from the mixed liquor during treatment in the first nitrogen removal stage by passing mixed liquor containing BOD from the first nitrogen removal stage to the second nitrogen removal stage and utilizing BOD that has passed through the first nitrogen removal stage in the anoxic zone of the second nitrogen removal stage to effectuate further denitrification.

17. The method of claim 16 including the step of transferring the BOD containing mixed liquor into the anoxic stage of the first nitrogen removal stage and transferring BOD containing mixed liquor from the first anoxic zone to the second anoxic zone before the BOD associated with the mixed liquor is depleted, thereby providing for the use of BOD in the second anoxic zone to effectuate denitrification.

18. The method of claim 1 wherein the formed mixed liquor is first introduced into the anoxic zone of the first nitrogen removal stage.

19. The method of claim 1 wherein the formed mixed liquor is first introduced into the aerobic zone of the first nitrogen removal stage.

20. An activated sludge process for biologically removing BOD and nitrogen from wastewater comprising the steps of:

(a) forming mixed liquor;

(b) transferring the mixed liquor through a plurality of nitrogen removal stages by directing the mixed liquor into a first anoxic zone of a first nitrogen removal stage and maintaining the mixed liquor under anoxic conditions for a specified period to permit denitrifying organisms to reduce a portion of the nitrates and nitrites present in the mixed liquor to elemental nitrogen, transferring a portion of the mixed liquor from the first anoxic zone to a first aerobic zone in the first nitrogen removal stage and aerating the mixed liquor for a sufficient time period for nitrifying organisms to convert a portion of the ammonia and organic nitrogen in the mixed liquor into nitrates and nitrites, and recycling the mixed liquor back and forth between the first anoxic zone and the first aerobic zone of the first nitrogen removal stage to effectuate denitrification and nitrification;

(c) transferring mixed liquor from the first anoxic zone to a second anoxic zone of a second nitrogen removal stage and denitrifying the mixed liquor, transferring the mixed liquor from the second anoxic zone to a second aerobic zone and nitrifying the mixed liquor within the second aerobic zone, and recycling the mixed liquor back and forth between the second anoxic zone and the second aerobic zone of the second stage to effectuate further denitrification and nitrification;

(d) transferring the mixed liquor treated in the first and second nitrogen removal stages to a final clarifier where settled sludge is separated from purified supernatant; and

(e) recycling at least a portion of the settled sludge to form the mixed liquor.

21. An activated sludge process for biologically removing BOD and nitrogen from wastewater comprising the steps of:

(a) forming mixed liquor;

(b) transferring the mixed liquor through a series of nitrogen removal stages by directing the mixed liquor into a first anoxic zone of a first nitrogen removal stage and maintaining the mixed liquor under anoxic conditions for a specified period to permit denitrifying organisms to reduce a portion of the nitrates and nitrites present in the mixed liquor to elemental nitrogen, transferring a portion of the mixed liquor from the first anoxic zone to a first aerobic zone within the first nitrogen removal stage and aerating the mixed liquor for a sufficient time period for nitrifying organisms to convert a portion of the ammonia and organic nitrogen in the mixed liquor into nitrates and nitrites, and recycling the mixed liquor back and forth between the first anoxic zone and the first aerobic zone of the first nitrogen removal stage to effectuate denitrification and nitrification;

(c) transferring mixed liquor from the first aerobic zone to a second aerobic zone of a second nitrogen removal stage and nitrifying the mixed liquor therein, transferring the mixed liquor from the second aerobic zone to a second anoxic zone within the second nitrogen removal zone and denitrifying the mixed liquor in the second anoxic zone, and recycling the mixed liquor back and forth between the second aerobic zone and the second anoxic zone of the second stage to effectuate further nitrification and denitrification;

(d) transferring the mixed liquor treated in the first and second nitrogen removal stages to a final clarifier where settled sludge is separated from purified supernatant; and

(e) recycling at least a portion of the settled sludge to form the mixed liquor.